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Production of resistant starch product having tailored degree of polymerization

Production of resistant starch product having tailored degree of polymerization description/claims

This application claims priority from U.S. provisional patent application Ser. No. 60/894,825, filed on Mar. 14, 2007, and U.S. provisional patent application Ser. No. 60/893,160, filed on Mar. 6, 2007, both of which are incorporated herein by reference.

Starch comprises two polysaccharides: amylose and amylopectin. Amylose is a generally linear polymer that comprises glucose units connected by alpha 1-4 glycosidic linkages. Amylopectin is a branched polymer in which many of the glucose units are connected by alpha 1-4 glycosidic linkages, but some are connected by alpha 1-6 glycosidic linkages.

Alpha-amylase is an enzyme that is present in the human body and which hydrolyzes alpha 1-4 linkages in starch, thus leading to digestion of the starch. In certain situations it is desirable to produce starch that resists hydrolysis by alpha-amylase, for example to decrease the caloric content of the starch, or to increase its dietary fiber content. However, attempts to produce such starch in the past have suffered from one or more problems, such as high cost.

Amylase-resistant starch is usually produced from high-amylose starch, which is often expensive. There is a need for improved processes for producing starch with a high content of amylose that is suitable for production of alpha-amylase resistant starch.

One embodiment of the invention is a process for producing a starch product that comprises (a) treating a feed starch with glucanotransferase to produce a chain-extended starch; and (b) treating the chain-extended starch with a debranching enzyme to produce a starch product that comprises amylose fragments. Further embodiments comprise one or more of (c) crystallizing at least part of the starch product; (d) heating the starch product in the presence of moisture; (e) treating the starch product with alpha-amylase; (f) washing the starch product to remove at least some non-crystallized starch; and spray drying the debranched starch product, wherein the degree of polymerization of the starch product is increased by increasing the amylose content of the feed starch or is decreased by decreasing the amylose content of the feed starch.

The process can also comprise recovering the remaining starch product after it has been washed. In some embodiments of the process, the feed starch is heated to at least partially gelatinize it prior to treatment with glucanotransferase.

In some embodiments of the process, at least about 38% by weight of the starch product comprises amylose fragments that have a degree of polymerization (DP) of at least about 35. The process can optionally further include recovering the amylose fragments. As another option, the process can include membrane filtering a solution or dispersion of the starch product to increase the concentration of amylose fragments that have a degree of polymerization (DP) of at least about 35.

Another embodiment of the present invention is a process for producing a starch product that comprises treating a feed starch with glucanotransferase to produce a chain-extended starch; treating the chain-extended starch with a debranching enzyme to produce a starch product that comprises amylose fragments; crystallizing at least part of the starch product; heating the starch product in the presence of moisture; and washing the starch product to remove at least some non-crystallized starch, wherein the degree of polymerization of the starch product is increased by increasing the amylose content of the feed starch or is decreased by decreasing the amylose content of the feed starch. Other than the absence of treatment with alpha-amylase, various embodiments of this process can be similar to or the same as those of the above-described process.

Another embodiment of the present invention is a starch product produced by any of the above-described processes. In some embodiments of the invention, at least about 40% by weight of the amylose fragments have a degree of polymerization (DP) of at least about 35. If the process used to make the starch product includes membrane filtration, then in some embodiments at least about 50% by weight of the amylose fragments have a degree of polymerization (DP) of at least about 35. In some instances the starch product has a peak melting temperature of greater than about 105° C.

Another embodiment of the invention is a food product that contains the above-described starch product.

One embodiment of the present invention is a process of producing starch having a relatively high content of amylose. This process includes treating a feed starch that comprises amylopectin with glucanotransferase to extend at least some of the starch chains, and treating the chain-extended starch with a debranching enzyme to produce amylose fragments. These amylose fragments can then be crystallized to produce a resistant starch product.

Ordinary dent corn starch can be debranched enzymatically to give short chain amylose fragments, but since the amylopectin component of the starch is usually composed of relatively short branched chains, the product contains too few of the longer chain lengths that are needed for enzyme resistance. Debranched dent corn starch that has not been modified with a glucanotransferase typically contains less than 35% of the DP35 and higher chain lengths (i.e., starch molecules having a degree of polymerization of at least 35) and therefore does not have the thermal stability needed for a resistant starch. In addition, the debranched dent starch contains a fraction of long chain lengths from amylose as well as short chains from amylopectin. This combination of heterogeneous chain lengths is not optimal for crystallization and amylase resistance.

The feed starch used in the present process can come from a variety of sources, including dent corn, waxy corn, high amylose ae genetic corn (ae is the name of a genetic mutation commonly known by corn breeders and is short for “amylose extender”), potato, tapioca, rice, pea, wheat, waxy wheat, as well as purified amylose from these starches, and alpha-1,4 glucans produced according to patent application WO 00/14249, which is incorporated herein by reference, and combinations of two or more of these starch sources. Chemically modified starches, such as hydroxypropyl starches, starch adipates, acetylated starches, and phosphorylated starches, can also be used in the present invention. For example, suitable chemically modified starches include, but are not limited to, crosslinked starches, acetylated and organically esterified starches, hydroxyethylated and hydroxypropylated starches, phosphorylated and inorganically esterified starches, cationic, anionic, nonionic, and zwitterionic starches, and succinate and substituted succinate derivatives of starch. Such modifications are known in the art, for example in Modified Starches: Properties and Uses, Ed. Wurzburg, CRC Press, Inc., Florida (1986). Other suitable modifications and methods are disclosed in U.S. Pat. Nos. 4,626,288, 2,613,206 and 2,661,349, which are incorporated herein by reference.

If the feed starch is a waxy starch, it can be at least partially debranched by treatment with a debranching enzyme prior to treatment with glucanotransferase. Suitable debranching enzymes for this purpose include pullulanase and isoamylase. This provides a source of fragments that will be transferred by the glucanotransferase to the amylopectin non-reducing ends, resulting in longer branched chains.

An improved resistant starch, with a more tailored degree of polymerization (DP) than that observed with use of dent corn starch alone, can be produced by modifying the feed starch, as will be described below.

For longer DP than that obtained by treating regular dent corn starch alone, amylose can be added, for example, amylose isolated from dent starch or high amylose starch. The DP correlates with the proportion of amylose in the feed starch, e.g., the longer the desired DP of the product, the greater the proportion of amylose that can be chosen for the feed starch. Using only a small amount of added amylose would result in only a small increase in DP compared to that obtained with dent corn starch alone.

• Provisional Patent
• Utility Patent

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